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The article contains sections titled: 1. Introduction 2. Properties 2.1. Physical Properties 2.2. Chemical Properties 3. Development of the Sulfuric Acid Industry 3.1. Early Development 3.2. Further Development of the Nitrogen Oxide Process 3.3. Ascendency of the Contact Process 3.4. Raw Materials Usage 4. Production 4.1. Production by Contact Processes 4.1.1. Reaction Kinetics and Thermodynamics 4.1.2. Catalysts 4.1.3. Process Summary 4.1.3.1. Gas Drying 4.1.3.2. Catalytic Oxidation of Sulfur Dioxide 4.1.3.3. Absorption of Sulfur Trioxide 4.1.3.4. Acid Cooling 4.1.4. Practical Versions of the Contact Process 4.1.4.1. Double‐Absorption Process Based on Sulfur Combustion 4.1.4.2. Double‐Absorption Processes Based on Metallurgical Gases 4.1.4.3. Ordinary Single‐Absorption Processes 4.1.4.4. Wet‐Catalysis Processes 4.1.5. Tail‐Gas Treatment 4.1.6. Economic Factors 4.2. Production by Nitrogen Oxide Processes 4.3. Regeneration of Spent Sulfuric Acid 4.3.1. Introduction 4.3.2. Reconcentration to 70 ‐ 75 % H 2 SO 4 4.3.3. Concentration to 93 ‐ 98 % H 2 SO 4 4.4. Production of Oleum 5. Construction Materials 5.1. Metallic Materials 5.2. Nonmetallic Materials 6. Uses of Sulfuric Acid and Economic Aspects 6.1. Indirect Uses 6.2. Direct Uses 6.3. Economic Aspects 7. Analytical Techniques 7.1. Concentration Measurement 7.2. Measurement of Impurities 7.3. Analysis of Acid‐Plant Gas Streams 8. Sulfur Trioxide 8.1. Properties 8.2. Manufacture 8.3. Handling and Uses 9. Toxicology 9.1. Sulfuric Acid 9.2. Sulfur Trioxide 10. Acknowledgement
The article contains sections titled: 1. Introduction 2. Properties 2.1. Physical Properties 2.2. Chemical Properties 3. Development of the Sulfuric Acid Industry 3.1. Early Development 3.2. Further Development of the Nitrogen Oxide Process 3.3. Ascendency of the Contact Process 3.4. Raw Materials Usage 4. Production 4.1. Production by Contact Processes 4.1.1. Reaction Kinetics and Thermodynamics 4.1.2. Catalysts 4.1.3. Process Summary 4.1.3.1. Gas Drying 4.1.3.2. Catalytic Oxidation of Sulfur Dioxide 4.1.3.3. Absorption of Sulfur Trioxide 4.1.3.4. Acid Cooling 4.1.4. Practical Versions of the Contact Process 4.1.4.1. Double‐Absorption Process Based on Sulfur Combustion 4.1.4.2. Double‐Absorption Processes Based on Metallurgical Gases 4.1.4.3. Ordinary Single‐Absorption Processes 4.1.4.4. Wet‐Catalysis Processes 4.1.5. Tail‐Gas Treatment 4.1.6. Economic Factors 4.2. Production by Nitrogen Oxide Processes 4.3. Regeneration of Spent Sulfuric Acid 4.3.1. Introduction 4.3.2. Reconcentration to 70 ‐ 75 % H 2 SO 4 4.3.3. Concentration to 93 ‐ 98 % H 2 SO 4 4.4. Production of Oleum 5. Construction Materials 5.1. Metallic Materials 5.2. Nonmetallic Materials 6. Uses of Sulfuric Acid and Economic Aspects 6.1. Indirect Uses 6.2. Direct Uses 6.3. Economic Aspects 7. Analytical Techniques 7.1. Concentration Measurement 7.2. Measurement of Impurities 7.3. Analysis of Acid‐Plant Gas Streams 8. Sulfur Trioxide 8.1. Properties 8.2. Manufacture 8.3. Handling and Uses 9. Toxicology 9.1. Sulfuric Acid 9.2. Sulfur Trioxide 10. Acknowledgement
The sections in this article are Introduction The Contact Process Thermodynamic Considerations Reaction Mechanisms and Kinetics Sulfur Dioxide as the Basis of Sulfuric Acid Production Classical Sulfuric Acid Production Sulfur Dioxide from Combustion of Elemental Sulfur Sulfur Dioxide from Roasting of Pyrite Sulfur Dioxide from Metallurgical Plants Copper Smelting Zinc Blende Roasting Nickel Sulfide and Lead Sulfide Sulfur Dioxide from Decomposition of Acid Sulfur Dioxide from Combustion of H 2 S Sulfur Dioxide from Sulfates Decomposition of Gypsum ( M üller– K ühne Process) Decomposition of Iron Sulfate Sulfuric Acid from Sulfur Dioxide in Tail Gases from Power Stations The Contact Process: Practical Application Fundamentals Single Absorption Catalysis Double Absorption Catalysis Pressure Catalysis Fluidized‐Bed Technology The Catalyst Catalyst Production Catalyst Requirements Disposal of Spent Catalyst
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